EP4357386A1 - Poly(3-hydroxypropionic acid) block copolymer, preparation method therefor and product comprising same - Google Patents
Poly(3-hydroxypropionic acid) block copolymer, preparation method therefor and product comprising same Download PDFInfo
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- EP4357386A1 EP4357386A1 EP22853485.5A EP22853485A EP4357386A1 EP 4357386 A1 EP4357386 A1 EP 4357386A1 EP 22853485 A EP22853485 A EP 22853485A EP 4357386 A1 EP4357386 A1 EP 4357386A1
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- EP
- European Patent Office
- Prior art keywords
- hydroxypropionic acid
- poly
- weight
- lactone
- block copolymer
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- -1 Poly(3-hydroxypropionic acid) Polymers 0.000 title claims abstract description 128
- 229920001400 block copolymer Polymers 0.000 title claims abstract description 30
- 238000002360 preparation method Methods 0.000 title 1
- ALRHLSYJTWAHJZ-UHFFFAOYSA-N 3-hydroxypropionic acid Chemical compound OCCC(O)=O ALRHLSYJTWAHJZ-UHFFFAOYSA-N 0.000 claims abstract description 64
- JJTUDXZGHPGLLC-UHFFFAOYSA-N lactide Chemical compound CC1OC(=O)C(C)OC1=O JJTUDXZGHPGLLC-UHFFFAOYSA-N 0.000 claims abstract description 48
- 150000002596 lactones Chemical class 0.000 claims abstract description 40
- 239000000178 monomer Substances 0.000 claims abstract description 39
- 239000000126 substance Substances 0.000 claims description 34
- 238000000034 method Methods 0.000 claims description 21
- PAPBSGBWRJIAAV-UHFFFAOYSA-N ε-Caprolactone Chemical compound O=C1CCCCCO1 PAPBSGBWRJIAAV-UHFFFAOYSA-N 0.000 claims description 15
- 125000004432 carbon atom Chemical group C* 0.000 claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 10
- 230000000379 polymerizing effect Effects 0.000 claims description 10
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical compound O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 claims description 8
- 239000011347 resin Substances 0.000 claims description 8
- 229920005989 resin Polymers 0.000 claims description 8
- 239000011342 resin composition Substances 0.000 claims description 7
- IPBFYZQJXZJBFQ-UHFFFAOYSA-N gamma-octalactone Chemical compound CCCCC1CCC(=O)O1 IPBFYZQJXZJBFQ-UHFFFAOYSA-N 0.000 claims description 6
- 238000007151 ring opening polymerisation reaction Methods 0.000 claims description 6
- 239000000376 reactant Substances 0.000 claims description 5
- OZJPLYNZGCXSJM-UHFFFAOYSA-N 5-valerolactone Chemical compound O=C1CCCCO1 OZJPLYNZGCXSJM-UHFFFAOYSA-N 0.000 claims description 4
- GSCLMSFRWBPUSK-UHFFFAOYSA-N beta-Butyrolactone Chemical compound CC1CC(=O)O1 GSCLMSFRWBPUSK-UHFFFAOYSA-N 0.000 claims description 4
- GAEKPEKOJKCEMS-UHFFFAOYSA-N gamma-valerolactone Chemical compound CC1CCC(=O)O1 GAEKPEKOJKCEMS-UHFFFAOYSA-N 0.000 claims description 4
- 239000003999 initiator Substances 0.000 claims description 4
- 125000000217 alkyl group Chemical group 0.000 claims description 3
- JYVXNLLUYHCIIH-UHFFFAOYSA-N (+/-)-mevalonolactone Natural products CC1(O)CCOC(=O)C1 JYVXNLLUYHCIIH-UHFFFAOYSA-N 0.000 claims description 2
- VPVXHAANQNHFSF-UHFFFAOYSA-N 1,4-dioxan-2-one Chemical compound O=C1COCCO1 VPVXHAANQNHFSF-UHFFFAOYSA-N 0.000 claims description 2
- QTWLQDVFHKLZRA-UHFFFAOYSA-N 4-ethyloxetan-2-one Chemical compound CCC1CC(=O)O1 QTWLQDVFHKLZRA-UHFFFAOYSA-N 0.000 claims description 2
- OALYTRUKMRCXNH-UHFFFAOYSA-N 5-pentyloxolan-2-one Chemical compound CCCCCC1CCC(=O)O1 OALYTRUKMRCXNH-UHFFFAOYSA-N 0.000 claims description 2
- RZTOWFMDBDPERY-UHFFFAOYSA-N Delta-Hexanolactone Chemical compound CC1CCCC(=O)O1 RZTOWFMDBDPERY-UHFFFAOYSA-N 0.000 claims description 2
- JYVXNLLUYHCIIH-ZCFIWIBFSA-N R-mevalonolactone, (-)- Chemical compound C[C@@]1(O)CCOC(=O)C1 JYVXNLLUYHCIIH-ZCFIWIBFSA-N 0.000 claims description 2
- 238000001125 extrusion Methods 0.000 claims description 2
- 239000000835 fiber Substances 0.000 claims description 2
- 239000006260 foam Substances 0.000 claims description 2
- 238000002347 injection Methods 0.000 claims description 2
- 239000007924 injection Substances 0.000 claims description 2
- 229940057061 mevalonolactone Drugs 0.000 claims description 2
- 239000004745 nonwoven fabric Substances 0.000 claims description 2
- YFHICDDUDORKJB-UHFFFAOYSA-N trimethylene carbonate Chemical compound O=C1OCCCO1 YFHICDDUDORKJB-UHFFFAOYSA-N 0.000 claims description 2
- 230000000704 physical effect Effects 0.000 abstract description 6
- 229920002988 biodegradable polymer Polymers 0.000 abstract description 4
- 239000004621 biodegradable polymer Substances 0.000 abstract description 4
- 230000000052 comparative effect Effects 0.000 description 37
- 229920001577 copolymer Polymers 0.000 description 30
- 239000003054 catalyst Substances 0.000 description 24
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 8
- 238000002425 crystallisation Methods 0.000 description 8
- 230000008025 crystallization Effects 0.000 description 8
- 229920000642 polymer Polymers 0.000 description 8
- 238000005259 measurement Methods 0.000 description 6
- 230000035484 reaction time Effects 0.000 description 6
- 238000002474 experimental method Methods 0.000 description 5
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 3
- 229920000747 poly(lactic acid) Polymers 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- 238000002834 transmittance Methods 0.000 description 3
- 229930188620 butyrolactone Natural products 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 2
- 150000002148 esters Chemical group 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000691 measurement method Methods 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 238000006068 polycondensation reaction Methods 0.000 description 2
- 239000004626 polylactic acid Substances 0.000 description 2
- BOZRCGLDOHDZBP-UHFFFAOYSA-N 2-ethylhexanoic acid;tin Chemical compound [Sn].CCCCC(CC)C(O)=O BOZRCGLDOHDZBP-UHFFFAOYSA-N 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 229910052772 Samarium Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 125000003545 alkoxy group Chemical group 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000012661 block copolymerization Methods 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000000113 differential scanning calorimetry Methods 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000012776 electronic material Substances 0.000 description 1
- 239000003480 eluent Substances 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 229920001610 polycaprolactone Polymers 0.000 description 1
- 239000004632 polycaprolactone Substances 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920005604 random copolymer Polymers 0.000 description 1
- 238000007142 ring opening reaction Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 229910052727 yttrium Inorganic materials 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/02—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds
- C08G63/06—Polyesters derived from hydroxycarboxylic acids or from polycarboxylic acids and polyhydroxy compounds derived from hydroxycarboxylic acids
- C08G63/08—Lactones or lactides
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G63/00—Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
- C08G63/78—Preparation processes
Definitions
- the present disclosure relates to a poly(3-hydroxypropionic acid) block copolymer, a manufacturing method thereof and products containing the same .
- Poly(3-hydroxypropionic acid) is a biodegradable polymer, and has not only the property of not cracking easily but also excellent mechanical properties, and thus is attracting attention as an environmentally friendly material.
- Poly(3-hydroxypropionic acid) is produced by performing a polycondensation of 3-hydroxypropionic acid (3-HP) as a monomer. Considering industrial applicability, poly(3-hydroxypropionic acid) having excellent thermal stability should be produced. However, the chain of the poly(3-hydroxypropionic acid) contains an ester structure, and the ester structure has a thermal decomposition temperature of about 220°C, and therefore, there is a limit in improving thermal stability.
- poly(3-hydroxypropionic acid) having a high molecular weight can be produced to thereby improve a thermal stability, but in the process of polycondensation of 3-hydroxypropionic acid, a low molecular weight cyclic structure is generated, which not only makes it impossible to produce high molecular weight poly(3-hydroxypropionic acid), but also reduces the production yield of poly(3-hydroxypropionic acid).
- the present inventors have found that when lactone, lactide, or a combination thereof is added to 3-hydroxypropionic acid as a monomer to produce a copolymer, the thermal properties, crystallinity, and tensile properties of the produced biodegradable polymer can be controlled by varying the number of carbon atoms present in the lactone ring, the presence or absence of branches, and the type of branched chain, and completed the present disclosure.
- a poly(3-hydroxypropionic acid) block copolymer In order to achieve the above object, according to the present disclosure, provided is a poly(3-hydroxypropionic acid) block copolymer.
- the poly(3-hydroxypropionic acid) block copolymer according to the present disclosure comprises a repeating unit of the following Chemical Formula 1, which is a repeating unit of 3-hydroxypropionic acid; and a repeating unit of the following Chemical Formula 2, which is a repeating unit of lactone, wherein the number (m) of repeating units of the Chemical Formula 1 is an integer of 100 to 5000, wherein the number (n) of repeating units of the Chemical Formula 2 is an integer of 100 to 5000, and L in the Chemical Formula 2 is a linear or branched alkyl having 3 to 10 carbon atoms: [12]
- a method of manufacturing a poly(3-hydroxypropionic acid) block copolymer comprising polymerizing 3-hydroxypropionic acid to produce a 3-hydroxypropionic acid oligomer (step 1); polymerizing the 3-hydroxypropionic acid oligomer to produce poly(3-hydroxypropionic acid) (step 2); and performing a ring-opening polymerization of lactone having 3 to 10 carbon atoms using the poly(3-hydroxypropionic acid) as an initiator (step 3).
- the poly(3-hydroxypropionic acid) block copolymer according to the present disclosure has the characteristic that by introducing 3-hydroxypropionic acid and a lactone monomer or further an lactide monomer, various physical properties such as thermal properties, crystallinity and tensile properties of the biodegradable polymer can be improved, and its application fields can be expanded.
- the present disclosure aims at providing a poly(3-hydroxypropionic acid) block copolymer.
- the poly(3-hydroxypropionic acid) block copolymer of the present disclosure will be described in detail as follows.
- the poly(3-hydroxypropionic acid) block copolymer of the present disclosure comprises a repeating unit of the following Chemical Formula 1, which is a repeating unit of 3-hydroxypropionic acid; and a repeating unit of the following Chemical Formula 2, which is a repeating unit of lactone, wherein the number (m) of repeating units of the Chemical Formula 1 is an integer of 100 to 5000, wherein the number (n) of repeating units of the Chemical Formula 2 is an integer of 100 to 5000, and L in the Chemical Formula 2 is a linear or branched alkyl having 3 to 10 carbon atoms:
- poly(3-hydroxypropionic acid) block copolymer including the repeating unit of Chemical Formula 1 and the repeating unit of Chemical Formula 2 can be the following Chemical Formula 4.
- Chemical Formula 4 when ⁇ -caprolactone is used as lactone, which is the repeating unit of Chemical Formula 2, the Chemical Formula 4 can be represented by following Chemical Formula 4-1.
- Chemical Formula 4 can be represented by following Chemical Formula 4-2.
- the poly(3-hydroxypropionic acid) block copolymer further comprises a repeating unit of Chemical Formula 3, which is a repeating unit of lactide, and the number (I) of repeating units of Chemical Formula 3 can be an integer of 100 to 5000:
- poly(3-hydroxypropionic acid) block copolymer further comprising the repeating unit of Chemical Formula 3 can be the following Chemical Formula 5.
- 'poly(3-hydroxypropionic acid) 'block copolymer' is a block copolymer in which a lactone-derived monomer, a 3-hydroxypropionic acid-derived monomer and additionally a lactide-derived monomer are polymerized in block units.
- crystallization properties can be controlled in accordance with the number of carbon atoms present in the lactone ring and the presence or absence of introduction of a branched structure, thereby being capable of adjusting crystallization and tensile physical properties, etc.
- the present disclosure is characterized in that it necessarily includes 3-hydroxypropionic acid monomer, unlike conventional PLA (polylactic acid), and includes a lactone-derived monomer, a lactide-derived monomer, or a combination thereof.
- the present disclosure provides a method of manufacturing the above-mentioned poly(3-hydroxypropionic acid) block copolymer comprising a step of polymerizing 3-hydroxypropionic acid polymer and lactone using a catalyst.
- the 3-hydroxypropionic acid polymer means a homopolymer of 3-hydroxypropionic acid.
- the method for manufacturing poly(3-hydroxypropionic acid-b-lactone) of the present disclosure comprises polymerizing 3-hydroxypropionic acid to produce a 3-hydroxypropionic acid oligomer (step 1); polymerizing the 3-hydroxypropionic acid oligomer to produce poly(3-hydroxypropionic acid) (step 2); and performing a ring-opening polymerization of lactone having 3 to 10 carbon atoms using the poly(3-hydroxypropionic acid) as an initiator (step 3).
- the (step 3) can further include providing a lactide monomer.
- the lactide can be included in an amount of 40 parts by weight to 99 parts by weight based on 100 parts by weight of the total weight of lactone and lactide.
- the lactide can be included in an amount of 40 parts by weight or more, 50 parts by weight or more, 60 parts by weight or more, or 70 parts by weight or more and 99 parts by weight or less, 90 parts by weight or less, or 80 parts by weight or less based on 100 parts by weight of the total weight of lactone and lactide.
- the degree of improvement in thermal and mechanical properties of the block copolymer may not be significant if the lactide content is too low.
- the (step 3) can include polymerizing lactide using the poly(3-hydroxypropionic acid) as an initiator (step 3-1); and further performing a ring-opening polymerization of a lactone having 3 to 10 carbon atoms to poly(3-hydroxypropionic acid) and a lactide polymer (step 3-2). If lactide is polymerized first and then lactone is polymerized, a block copolymer can be obtained in which 3-hydroxypropionic acid-derived repeating units, lactide-derived repeating units, and lactone-derived repeating units are each polymerized to form a block. The block copolymer is different from the random copolymer in that it has higher crystallinity.
- lactone can be included in an amount of 1 part by weight to 60 parts by weight based on 100 parts by weight of the total weight of lactone and lactide.
- lactone can be included in an amount of 1 part by weight or more, 5 parts by weight or more, 10 parts by weight or more, or 20 parts by weight or more to 60 parts by weight or less, 50 parts by weight or less, 40 parts by weight or less, or 30 parts by weight or less based on 100 parts by weight of the total weight of lactone and lactide.
- poly(3-hydroxypropionic acid) can be included in an amount of 50 parts by weight or less based on 100 parts by weight of the total weight of the reactants.
- the reactants of the (step 3) can be poly(3-hydroxypropionic acid) and lactone or poly(3-hydroxypropionic acid), lactone and lactide.
- poly(3-hydroxypropionic acid) can be included in an amount of 50 parts by weight or less, 40 parts by weight or less, 30 parts by weight or less, 20 parts by weight or less, 17 parts by weight or less, or 10 parts by weight or less to more than 0 parts by weight, 5 parts by weight or more, or 9 parts by weight or more based on 100 parts by weight of the total weight of the reactants.
- the (step 2) is a step of polymerizing the 3-hydroxypropionic acid oligomer at a pressure of 1 torr or less for 12 hours to 48 hours.
- the polymerization is performed under a pressure of 0.2 torr or less for 22 hours to 26 hours.
- the lactone having 3 to 10 carbon atoms in (step 3) can be at least one selected from the group consisting of ⁇ -caprolactone, ⁇ -butyrolactone, ⁇ -valerolactone, ⁇ -butyrolactone, ⁇ -valerolactone, ⁇ -valerolactone, trimethylenecarbonate, p-dioxanone, ⁇ -haxalactone, ⁇ -caprolactone, mevalonolactone, ⁇ -octanoic lactone, and ⁇ -nonanoic lactone.
- the (step 3) is accompanied by a ring-opening polymerization reaction of lactone or further lactide, it is performed in the presence of a ring-opening catalyst.
- the catalyst can be a catalyst of the following Chemical Formula 2. [Chemical Formula 2] MA 1 p A 2 2-p wherein, Chemical Formula 2:
- the catalyst of Chemical Formula 2 can be tin(II) 2-ethylhexanoate (Sn(Oct) 2 ).
- the amount of the catalyst used can be 0.001 to 10 mol%, 0.01 to 5 mol%, 0.01 to 1 mol%, assuming that the total number of moles of lactone is 100 mol%.
- the (step 3) is performed at a temperature of 140 to 190°C.
- the manufacturing method is performed for 5 minutes to 10 hours, more preferably for 1 hour to 3 hours.
- the present disclosure can provide a resin comprising the above-mentioned poly(3-hydroxypropionic acid) block copolymer.
- the present disclosure can provide a resin composition comprising the resin.
- the resin composition can further include other additives for improving physical properties in addition to the resin.
- the resin composition can be molded into one or more resin molded articles selected from the group consisting of an injection molded article, an extrusion molded article, a blow molded article, an inflation, a fiber, a nonwoven fabric, a foam, a sheet, and like.
- the present disclosure provides an article comprising the above-mentioned poly(3-hydroxypropionic acid) block copolymer.
- the article can be an electronic material, a building material, a food packaging, a food container (disposable cup, tray, etc.), an industrial article, an agricultural article (e.g., mulching film), and the like.
- a resin, a resin composition, and an article comprising the poly(3-hydroxypropionic acid) block copolymer can further include two or more different types of lactones or additional comonomers depending on the required physical properties.
- 3-Hydroxypropionic acid present in an aqueous solution was dried at 90°C and 100 torr to obtain 60 g of dried 3-hydroxypropionic acid.
- 0.2 mol% of catalyst p-TSA p-toluenesulfonic acid
- the degree of vacuum was changed to 0.2 torr and reaction was performed for 5 hours, and then 0.05 mol% of Sn(Oct) 2 catalyst was added and reacted for a total of 24 hours to obtain a poly(3-hydroxypropionic acid) oligomer.
- the catalyst Sn(Oct) 2 (17 ⁇ l, 0.03 mol%) was added to the vacuum-dried poly(3-hydroxypropionic acid) (2g) of Comparative Example 1 and the dried ⁇ -caprolactone (20g), and reacted at 140°C for 3 hours to polymerize a copolymer.
- the polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and the product was taken out from a reactor and devolatilized at 50°C for 4 hours to remove residual monomers.
- the dried lactide (40 g) and catalyst Sn(Oct) 2 (11 ⁇ l, 0.01 mol%) were added to octanol (109 ⁇ l, 0.2 mol%) and reacted at 180°C for 1 hour. Then, ⁇ -caprolactone (7.9 g) was added thereto and reacted at 180°C for 1 hour to polymerize the copolymer.
- the polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 50°C for 4 hours to remove residual monomers.
- Measurements were performed under nitrogen gas flow using TA DSC250 model equipment. The temperature was raised from 40°C to 220°C at 5°C/min (1st heating), and the temperature was maintained at 220°C for 10 minutes. Then, it was cooled from 220°C to -70°C at 5°C/min (1st cooling), and the temperature was maintained at -70°C for 10 minutes. Then, the temperature was raised from -70°C to 220°C at 5°C/min (2nd heating) for measurement.
- Comparing Comparative Example 4 and Example 5 it was confirmed that the crystallization rate of Example 5 increased (the amount of change in enthalpy of T c increased from 2.8 J/g to 7.5 J/g), and the enthalpy decreased from 30.1 J/g to 15.1 J/g in cold crystallization. Also compared with Comparative Example 1, it was confirmed that poly(3-hydroxypropionic acid) is imparted with the thermal properties of polylactone and polylactide.
- Example 9 when lactide is included in an amount of 50 parts by weight based on 100 parts by weight of the total weight of lactone and lactide (Examples 7 and 9), it was confirmed that Example 9, in which the lactide monomer was block-polymerized, showed crystallinity, whereas in Example 7 in which the lactide monomer was randomly polymerized, the Tm was not measured, and it did not show crystallinity and had a gum-like state. In the case of Example 9 block-polymerized with the same composition, the crystallinity was lowered ( ⁇ H of Tm was 12.6 J/g), but Tm was measured.
- Example 6 in which lactide monomer was randomly polymerized, ⁇ H of Tm was measured as 19.2 J/g, which is low in crystallinity as compared to that of block-polymerized Example 8 in which ⁇ H of Tm is 5.7 J / g.
- the dog-bone mold was preheated in a heated hot press for 2 minutes, and then the polymer was injected, and processed for 2 minutes to prepare a dog-bone.
- the hot press temperature was set to 90°C
- Comparative Examples 2, 4 to 6 and Examples 5 to 9 the hot press temperature was set to 180°C.
- the dog-bone standard was set to length (64 cm), width (1 cm, 0.3 cm), and thickness (1 mm) according to ASTM 638.
- the specimen was pulled at a speed of 5 mm/min using an Instron 5982 model instrument using a weight of 5 kN, and the strength, elastic modulus, and elongation were measured.
- Example 2 and 4 showed that through a block copolymerization between poly(3-hydroxypropionic acid) and caprolactam, the tensile strength was increased to 20 MPa or more and the elongation was significantly increased to 600% or more.
- Examples 2 and 4 in which a weight average molecular weight was 100,000 g/mol or more, were excellent in both strength and elongation.
- Example 1 had the same monomer composition, catalyst type, use amount, and reaction temperature as Example 2, but the reaction time was 3 hours, which had a shorter reaction time than Example 2.
- Example 1 the tensile strength and elongation of Example 1 were shown inferior to those of Example 2, which is because the molecular weight of Example 1, which has a short reaction time, is small and thus entanglement between chains is small.
- Example 3 also had the same monomer composition, catalyst type, use amount and reaction temperature as Example 4, but the reaction time was 3 hours which is the shorter reaction time than Example 4. Therefore, the tensile strength and elongation of Example 3 were showed inferior to those of Example 4, which is because the molecular weight of Example 3, which also has a short reaction time, is small and thus entanglement between chains is small.
- Example 5 Comparing Comparative Example 4 and Example 5, it was confirmed that in Example 5, butyrolactone was block-copolymerized with poly (3-hydroxypropionic acid), and thus, the thermal processability was improved as compared to Comparative Example 4 in which thermal processing was impossible due to its brittleness. In addition, in Example 5, the copolymerized butyrolactone had a harder property than lactide, and thus the elongation was measured to be very low.
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- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
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- Polyesters Or Polycarbonates (AREA)
- Biological Depolymerization Polymers (AREA)
Abstract
A poly(3-hydroxypropionic acid) block copolymer having the characteristic that by introducing 3-hydroxypropionic acid and a lactone monomer or further an lactide monomer, various physical properties such as thermal properties, crystallinity and tensile properties of the biodegradable polymer are improved, and its application fields are expanded.
Description
- This application is a National Stage Application of International Application No.
PCT/KR2022/011553 filed on August 4, 2022 Korean Patent Application No. 10-2021-0102547 filed on August 4, 2021 Korean Patent Application No. 10-2022-0096678 filed on August 3, 2022 - The present disclosure relates to a poly(3-hydroxypropionic acid) block copolymer, a manufacturing method thereof and products containing the same .
- Poly(3-hydroxypropionic acid) is a biodegradable polymer, and has not only the property of not cracking easily but also excellent mechanical properties, and thus is attracting attention as an environmentally friendly material.
- Poly(3-hydroxypropionic acid) is produced by performing a polycondensation of 3-hydroxypropionic acid (3-HP) as a monomer. Considering industrial applicability, poly(3-hydroxypropionic acid) having excellent thermal stability should be produced. However, the chain of the poly(3-hydroxypropionic acid) contains an ester structure, and the ester structure has a thermal decomposition temperature of about 220°C, and therefore, there is a limit in improving thermal stability.
- In addition, poly(3-hydroxypropionic acid) having a high molecular weight can be produced to thereby improve a thermal stability, but in the process of polycondensation of 3-hydroxypropionic acid, a low molecular weight cyclic structure is generated, which not only makes it impossible to produce high molecular weight poly(3-hydroxypropionic acid), but also reduces the production yield of poly(3-hydroxypropionic acid).
- Therefore, the present inventors have found that when lactone, lactide, or a combination thereof is added to 3-hydroxypropionic acid as a monomer to produce a copolymer, the thermal properties, crystallinity, and tensile properties of the produced biodegradable polymer can be controlled by varying the number of carbon atoms present in the lactone ring, the presence or absence of branches, and the type of branched chain, and completed the present disclosure.
- It is an object of the present disclosure to provide a poly(3-hydroxypropionic acid) block copolymer having controlled thermal properties and tensile properties while maintaining the intrinsic properties of polypropionic acid, and a manufacturing method thereof.
- In order to achieve the above object, according to the present disclosure, provided is a poly(3-hydroxypropionic acid) block copolymer.
- The poly(3-hydroxypropionic acid) block copolymer according to the present disclosure comprises a repeating unit of the following Chemical Formula 1, which is a repeating unit of 3-hydroxypropionic acid; and a repeating unit of the following Chemical Formula 2, which is a repeating unit of lactone, wherein the number (m) of repeating units of the Chemical Formula 1 is an integer of 100 to 5000, wherein the number (n) of repeating units of the Chemical Formula 2 is an integer of 100 to 5000, and L in the Chemical Formula 2 is a linear or branched alkyl having 3 to 10 carbon atoms:
[12] - Also, provided is a method of manufacturing a poly(3-hydroxypropionic acid) block copolymer according to the present disclosure, comprising polymerizing 3-hydroxypropionic acid to produce a 3-hydroxypropionic acid oligomer (step 1); polymerizing the 3-hydroxypropionic acid oligomer to produce poly(3-hydroxypropionic acid) (step 2); and performing a ring-opening polymerization of lactone having 3 to 10 carbon atoms using the poly(3-hydroxypropionic acid) as an initiator (step 3).
- As described above, the poly(3-hydroxypropionic acid) block copolymer according to the present disclosure has the characteristic that by introducing 3-hydroxypropionic acid and a lactone monomer or further an lactide monomer, various physical properties such as thermal properties, crystallinity and tensile properties of the biodegradable polymer can be improved, and its application fields can be expanded.
- The present disclosure aims at providing a poly(3-hydroxypropionic acid) block copolymer. Hereinafter, the poly(3-hydroxypropionic acid) block copolymer of the present disclosure will be described in detail as follows.
- First, the poly(3-hydroxypropionic acid) block copolymer of the present disclosure comprises a repeating unit of the following Chemical Formula 1, which is a repeating unit of 3-hydroxypropionic acid; and a repeating unit of the following Chemical Formula 2, which is a repeating unit of lactone, wherein the number (m) of repeating units of the Chemical Formula 1 is an integer of 100 to 5000, wherein the number (n) of repeating units of the Chemical Formula 2 is an integer of 100 to 5000, and L in the Chemical Formula 2 is a linear or branched alkyl having 3 to 10 carbon atoms:
-
-
-
-
-
- The term 'poly(3-hydroxypropionic acid) 'block copolymer' as used herein is a block copolymer in which a lactone-derived monomer, a 3-hydroxypropionic acid-derived monomer and additionally a lactide-derived monomer are polymerized in block units. In particular, according to the present disclosure, by introducing a lactone-derived monomer, crystallization properties can be controlled in accordance with the number of carbon atoms present in the lactone ring and the presence or absence of introduction of a branched structure, thereby being capable of adjusting crystallization and tensile physical properties, etc.
- In addition, the present disclosure is characterized in that it necessarily includes 3-hydroxypropionic acid monomer, unlike conventional PLA (polylactic acid), and includes a lactone-derived monomer, a lactide-derived monomer, or a combination thereof.
- Further, the present disclosure provides a method of manufacturing the above-mentioned poly(3-hydroxypropionic acid) block copolymer comprising a step of polymerizing 3-hydroxypropionic acid polymer and lactone using a catalyst.
- The 3-hydroxypropionic acid polymer means a homopolymer of 3-hydroxypropionic acid.
- Specifically, the method for manufacturing poly(3-hydroxypropionic acid-b-lactone) of the present disclosure comprises polymerizing 3-hydroxypropionic acid to produce a 3-hydroxypropionic acid oligomer (step 1); polymerizing the 3-hydroxypropionic acid oligomer to produce poly(3-hydroxypropionic acid) (step 2); and performing a ring-opening polymerization of lactone having 3 to 10 carbon atoms using the poly(3-hydroxypropionic acid) as an initiator (step 3).
- The (step 3) can further include providing a lactide monomer.
- When lactide is further included as a monomer in (step 3), the lactide can be included in an amount of 40 parts by weight to 99 parts by weight based on 100 parts by weight of the total weight of lactone and lactide. For example, the lactide can be included in an amount of 40 parts by weight or more, 50 parts by weight or more, 60 parts by weight or more, or 70 parts by weight or more and 99 parts by weight or less, 90 parts by weight or less, or 80 parts by weight or less based on 100 parts by weight of the total weight of lactone and lactide.
- When lactide is further included as a monomer, the degree of improvement in thermal and mechanical properties of the block copolymer may not be significant if the lactide content is too low.
- Further, when lactide is further included as a monomer in the (step 3), the (step 3) can include polymerizing lactide using the poly(3-hydroxypropionic acid) as an initiator (step 3-1); and further performing a ring-opening polymerization of a lactone having 3 to 10 carbon atoms to poly(3-hydroxypropionic acid) and a lactide polymer (step 3-2). If lactide is polymerized first and then lactone is polymerized, a block copolymer can be obtained in which 3-hydroxypropionic acid-derived repeating units, lactide-derived repeating units, and lactone-derived repeating units are each polymerized to form a block. The block copolymer is different from the random copolymer in that it has higher crystallinity.
- Meanwhile, lactone can be included in an amount of 1 part by weight to 60 parts by weight based on 100 parts by weight of the total weight of lactone and lactide. For example, lactone can be included in an amount of 1 part by weight or more, 5 parts by weight or more, 10 parts by weight or more, or 20 parts by weight or more to 60 parts by weight or less, 50 parts by weight or less, 40 parts by weight or less, or 30 parts by weight or less based on 100 parts by weight of the total weight of lactone and lactide.
- In the (step 3), poly(3-hydroxypropionic acid) can be included in an amount of 50 parts by weight or less based on 100 parts by weight of the total weight of the reactants. The reactants of the (step 3) can be poly(3-hydroxypropionic acid) and lactone or poly(3-hydroxypropionic acid), lactone and lactide. Specifically, in the (step 3), poly(3-hydroxypropionic acid) can be included in an amount of 50 parts by weight or less, 40 parts by weight or less, 30 parts by weight or less, 20 parts by weight or less, 17 parts by weight or less, or 10 parts by weight or less to more than 0 parts by weight, 5 parts by weight or more, or 9 parts by weight or more based on 100 parts by weight of the total weight of the reactants.
- If the content of poly (3-hydroxypropionic acid) does not satisfy the above range, there can be minor problems that the effect of improving various physical properties such as thermal properties, crystallinity, and tensile properties due to the use of lactone can be insignificant.
- The (step 2) is a step of polymerizing the 3-hydroxypropionic acid oligomer at a pressure of 1 torr or less for 12 hours to 48 hours. Preferably, the polymerization is performed under a pressure of 0.2 torr or less for 22 hours to 26 hours.
- The lactone having 3 to 10 carbon atoms in (step 3) can be at least one selected from the group consisting of ε-caprolactone, β-butyrolactone, β-valerolactone, γ-butyrolactone, δ-valerolactone, γ-valerolactone, trimethylenecarbonate, p-dioxanone, δ-haxalactone, δ-caprolactone, mevalonolactone, γ-octanoic lactone, and γ-nonanoic lactone.
- Since the (step 3) is accompanied by a ring-opening polymerization reaction of lactone or further lactide, it is performed in the presence of a ring-opening catalyst. As an example, the catalyst can be a catalyst of the following Chemical Formula 2.
[Chemical Formula 2] MA1 pA2 2-p
wherein, Chemical Formula 2: - M is Al, Mg, Zn, Ca, Sn, Fe, Y, Sm, Lu, Ti or Zr;
- p is an integer of 0 to 2; and
- A1 and A2 are each independently an alkoxy or carboxyl group.
- More specifically, the catalyst of Chemical Formula 2 can be tin(II) 2-ethylhexanoate (Sn(Oct)2).
- Preferably, the amount of the catalyst used can be 0.001 to 10 mol%, 0.01 to 5 mol%, 0.01 to 1 mol%, assuming that the total number of moles of lactone is 100 mol%.
- Preferably, the (step 3) is performed at a temperature of 140 to 190°C. Preferably, the manufacturing method is performed for 5 minutes to 10 hours, more preferably for 1 hour to 3 hours.
- Further, the present disclosure can provide a resin comprising the above-mentioned poly(3-hydroxypropionic acid) block copolymer.
- Further, the present disclosure can provide a resin composition comprising the resin. The resin composition can further include other additives for improving physical properties in addition to the resin.
- Further, the resin composition can be molded into one or more resin molded articles selected from the group consisting of an injection molded article, an extrusion molded article, a blow molded article, an inflation, a fiber, a nonwoven fabric, a foam, a sheet, and like.
- Further, the present disclosure provides an article comprising the above-mentioned poly(3-hydroxypropionic acid) block copolymer. The article can be an electronic material, a building material, a food packaging, a food container (disposable cup, tray, etc.), an industrial article, an agricultural article (e.g., mulching film), and the like.
- A resin, a resin composition, and an article comprising the poly(3-hydroxypropionic acid) block copolymer can further include two or more different types of lactones or additional comonomers depending on the required physical properties.
- The present disclosure is described in more detail with reference to examples below. However, the following examples is for illustrative purposes only, and are not intended to limit the contents of the present disclosure.
- 3-Hydroxypropionic acid present in an aqueous solution was dried at 90°C and 100 torr to obtain 60 g of dried 3-hydroxypropionic acid. 0.2 mol% of catalyst p-TSA (p-toluenesulfonic acid) was added to the dried 3-hydroxypropionic acid, and the mixture was reacted at 90°C and 10 torr for 2 hours. Then, the degree of vacuum was changed to 0.2 torr and reaction was performed for 5 hours, and then 0.05 mol% of Sn(Oct)2 catalyst was added and reacted for a total of 24 hours to obtain a poly(3-hydroxypropionic acid) oligomer.
- The catalyst Sn(Oct)2 (17 µl, 0.03 mol%) was added to the vacuum-dried poly(3-hydroxypropionic acid) (2g) of Comparative Example 1 and the dried ε-caprolactone (20g), and reacted at 140°C for 3 hours to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and the product was taken out from a reactor and devolatilized at 50°C for 4 hours to remove residual monomers.
- The vacuum-dried poly(3-hydroxypropionic acid) (2 g) of Comparative Example 1 and the dried ε-caprolactone (20 g) were placed in a reactor. Then, catalyst Sn(Oct)2 (17 µl , 0.03 mol%) was added thereto and reacted at 140°C for 4 hours to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 50°C for 4 hours to remove residual monomers.
- The vacuum-dried poly(3-hydroxypropionic acid) (4 g) of Comparative Example 1 and the dried ε-caprolactone (20 g) were placed in a reactor. Then, catalyst Sn(Oct)2 (17 µl , 0.03 mol%) was added thereto and reacted at 140°C for 4 hours to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 50°C for 4 hours to remove residual monomers.
- The vacuum-dried poly(3-hydroxypropionic acid) (4 g) of Comparative Example 1 and the dried ε-caprolactone (20 g) were placed in a reactor. Then, catalyst Sn(Oct)2 (17 µl , 0.03 mol%) was added thereto and reacted at 140°C for 5 hours to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 50°C for 4 hours to remove residual monomers.
- The vacuum-dried poly(3-hydroxypropionic acid) (1.88 g) of Comparative Example 1, the dried β-butyrolactone (3.84 g) and the dried lactide (15 g) were placed in a reactor. Then, catalyst Sn(Oct)2 (14 µl , 0.03 mol%) was added thereto and reacted at 180°C for 1.5 hours to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 140°C for 4 hours to remove residual monomers.
- The vacuum-dried poly(3-hydroxypropionic acid) (2 g) of Comparative Example 1, the dried ε-caprolactone (4 g) and the dried lactide (16 g) were placed in a reactor. Then, catalyst Sn(Oct)2 (14 µl , 0.03 mol%) was added thereto and reacted at 180°C for 1 hour to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 50°C for 4 hours to remove residual monomers.
- The vacuum-dried poly(3-hydroxypropionic acid) (2 g) of Comparative Example 1, the dried ε-caprolactone (10 g) and the dried lactide (10 g) were placed in a reactor. Then, catalyst Sn(Oct)2 (15 µl , 0.03 mol%) was added thereto and reacted at 180°C for 1.5 hours to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 50°C for 4 hours to remove residual monomers.
- The vacuum-dried poly(3-hydroxypropionic acid) (2 g) of Comparative Example 1 and the dried lactide (16 g) were placed in a reactor. Then, catalyst Sn(Oct)2 (14 µl , 0.03 mol%) was added thereto and reacted at 180°C for 0.5 hour. Then, the dried ε-caprolactone (4 g) was added thereto and reacted for an additional 0.5 hours to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 50°C for 4 hours to remove residual monomers.
- The vacuum-dried poly(3-hydroxypropionic acid) (2 g) of Comparative Example 1 and the dried lactide (10 g) were placed in a reactor. Then, catalyst Sn(Oct)2 (15 µl , 0.03 mol%) was added thereto and reacted at 180°C for 0.5 hour. Then, the dried ε-caprolactone (10 g) was added thereto and reacted for an additional 1 hour to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 50°C for 4 hours to remove residual monomers.
- The vacuum-dried poly(3-hydroxypropionic acid) (4 g) of Comparative Example 1 and the dried lactide (40 g) were placed in a reactor. Then, catalyst Sn(Oct)2 (18 µl , 0.03 mol%) was added thereto and reacted at 180°C for 1 hour to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 140°C for 4 hours to remove residual monomers.
- The dried ε-caprolactone (40 g) and catalyst Sn(Oct)2 (11 µl, 0.01 mol%) were added to octanol (110 µl, 0.2 mol%) and reacted at 140°C for 4 hours to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 140°C for 4 hours to remove residual monomers.
- The dried β-butyrolactone (5.2 g), the dried lactide (20 g) and catalyst Sn(Oct)2 (6 µl , 0.01 mol%) were added to octanol (140 µl, 0.2 mol%) and reacted at 180°C for 1 hour to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 140°C for 4 hours to remove residual monomers.
- The dried ε-caprolactone (7.9 g), the dried lactide (40 g) and catalyst Sn(Oct)2 (11 µl, 0.01 mol%) were added to octanol (109 µl, 0.2 mol%) and reacted at 190°C for 1 hour to polymerize a copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 50°C for 4 hours to remove residual monomers.
- The dried lactide (40 g) and catalyst Sn(Oct) 2 (11 µl, 0.01 mol%) were added to octanol (109 µl, 0.2 mol%) and reacted at 180°C for 1 hour. Then, ε-caprolactone (7.9 g) was added thereto and reacted at 180°C for 1 hour to polymerize the copolymer. The polymerized copolymer was vacuum-dried at room temperature for 2 hours in order to remove moisture absorbed during the process, and then the product was taken out from the reactor and devolatilized at 50°C for 4 hours to remove residual monomers.
- The molecular weight and thermal properties of the polymers prepared in Examples 1 to 9 and Comparative Examples 1 to 6 were measured, and shown in Table 1 below. This is to investigate how the thermal properties of the polymerized copolymer change with the addition of lactone or lactone and lactide as a comonomer to 3-hydroxypropionic acid as compared to the existing poly(3-hydroxypropionic acid), that is, how the thermal properties are controlled, and not to show that a specific polymer is inferior.
- Each measurement method is as follows.
- Water e2695 model equipment and Agilent Plgel mixed c and b columns were used. Chloroform was used as an eluent, measurement was performed at a flow rate of 1 ml/min at 40 degrees, and the relative molecular weight was measured using polystyrene as a standard. Samples were prepared at 4 mg/ml with chloroform as solvent, and 50 µl was injected for measurement.
- Measurements were performed under nitrogen gas flow using TA DSC250 model equipment. The temperature was raised from 40°C to 220°C at 5°C/min (1st heating), and the temperature was maintained at 220°C for 10 minutes. Then, it was cooled from 220°C to -70°C at 5°C/min (1st cooling), and the temperature was maintained at -70°C for 10 minutes. Then, the temperature was raised from -70°C to 220°C at 5°C/min (2nd heating) for measurement.
[Table 1] Entry GPC DSC analysis Mn (g/mol) Mw (g/mol) PDI Tc Tg Cold crystallization Tm Tempera ture (°C) ΔH (J/g) Temperat ure (°C) Temperat ure (°C) ΔH(J/g) Tempera ture (°C) ΔH(J/g) Comp. Ex. 1 13300 29000 2.18 32 65.2 -20 N.D N.D 71.9 69.4 Comp. Ex. 2 60200 164200 2.72 97.1 38.8 50.9 N.D N.D 174 41.0 Comp. Ex. 3 147900 220800 1.49 29.0 53.5 -54 N.D N.D 55.6 55.3 Comp. Ex. 4 31800 58600 2.16 96.2 2.8 53.2 108.55 30.1 167.0 36.7 Comp. Ex. 5 106200 183800 1.73 N.D N.D 20.9 91.15 2.8 158.4 14.05 Comp. Ex. 6 51800 55400 1.26 103 31.7 -40.6 N.D N.D 169.1 33.0 Ex. 1 58500 108000 1.85 32.2 43.1 -56.5 N.D N.D 54 42.1 Ex. 2 72100 136600 1.9 29.1 50.9 -55.0 N.D N.D 53.7 46.5 Ex. 3 33300 53400 1.9 27.9 52.3 -55.2 N.D N.D 52.2 47.7 Ex. 4 54400 105900 2.0 30.2 50.7 -52.7 N.D N.D 52.6 46.7 Ex. 5 27700 86000 3.1 84.4 7.5 38.1 80 15.1 163.8 36.5 Ex. 6 49100 124800 2.6 N.D N.D 29.9 99 20.1 149.4 19.2 Ex. 7 41100 101322 2.6 N.D N.D -10.3 N.D N.D N.D N.D Ex. 8 44600 138550 2.5 N.D N.D 29.4 90 17.4 158.3 5.7 Ex. 9 38800 93074 2.4 N.D N.D -17.7 63.9 8.8 143.1 12.6 *N.D: not measured - Comparing Comparative Examples 2 and 3 with Examples 2 to 4, measured Tg and Tm of Comparative Example 3 and Examples 2 to 4 were lower than Comparative Example 2, confirming that since the content of poly(3-hydroxypropionic acid) is 10 or 20 parts by weight based on 100 parts by weight of the total weight of the reactants, Examples 2 to 4 followed the thermal properties of Comparative Example 3, which is polycaprolactone. Therefore, it was confirmed that poly(3-hydroxypropionic acid) was imparted with the thermal properties of polylactone.
- Comparing Comparative Example 4 and Example 5, it was confirmed that the crystallization rate of Example 5 increased (the amount of change in enthalpy of Tc increased from 2.8 J/g to 7.5 J/g), and the enthalpy decreased from 30.1 J/g to 15.1 J/g in cold crystallization. Also compared with Comparative Example 1, it was confirmed that poly(3-hydroxypropionic acid) is imparted with the thermal properties of polylactone and polylactide.
- Comparing Comparative Examples 5 and 6 with Examples 6 to 9, when lactide is included in an amount of 80 parts by weight based on 100 parts by weight of total lactone and lactide (Examples 6 and 8), there was no significant difference between random polymerization and block polymerization of lactide monomers.
- However, when lactide is included in an amount of 50 parts by weight based on 100 parts by weight of the total weight of lactone and lactide (Examples 7 and 9), it was confirmed that Example 9, in which the lactide monomer was block-polymerized, showed crystallinity, whereas in Example 7 in which the lactide monomer was randomly polymerized, the Tm was not measured, and it did not show crystallinity and had a gum-like state. In the case of Example 9 block-polymerized with the same composition, the crystallinity was lowered (ΔH of Tm was 12.6 J/g), but Tm was measured.
- Comparing Examples 6 and 8, it was confirmed that in Example 6 in which lactide monomer was randomly polymerized, ΔH of Tm was measured as 19.2 J/g, which is low in crystallinity as compared to that of block-polymerized Example 8 in which ΔH of Tm is 5.7 J / g.
- Looking at Tg, Tm, cold crystallization (2nd heating result) and Tc (1st cooling result), it was confirmed that generally, if the crystallization rate is high, the enthalpy of Tc is large, and the temperature of cold crystallization is low or not measured, and if the crystallinity is high, the enthalpy of Tm is higher. If the crystallinity is high, generally, the strength of the material increases, but it is brittle and has no elasticity. However, since elasticity is generally known to be created by voids between polymer chains, the use of branched structures as monomers can lower crystallinity and reduce brittleness.
- The mechanical properties of the polymers prepared in Examples 1 to 9 and Comparative Examples 1 to 6 were measured and shown in Table 2 below.
- Each measurement method is as follows.
- The dog-bone mold was preheated in a heated hot press for 2 minutes, and then the polymer was injected, and processed for 2 minutes to prepare a dog-bone. At this time, in Comparative Examples 1, 3 and Examples 1 to 4, the hot press temperature was set to 90°C, and in Comparative Examples 2, 4 to 6 and Examples 5 to 9, the hot press temperature was set to 180°C. The dog-bone standard was set to length (64 cm), width (1 cm, 0.3 cm), and thickness (1 mm) according to ASTM 638.
- The specimen was pulled at a speed of 5 mm/min using an Instron 5982 model instrument using a weight of 5 kN, and the strength, elastic modulus, and elongation were measured.
- Each specimen was prepared as a sheet having the thickness shown in Table 2, and then transmittance was measured by attaching to a UV-visible spectrometer (Agilent 8453). At this time, the transmittance value in the 480nm region was confirmed.
[Table 2] Entry Dog-bone processability Mechanical properties Optical properties Tensile strength (MPa) Modulus (GPa) Elongation (%) Thickness Transmittance (%) Comparative Example 1 X N.A N.A N.A 200 77.7 Comparative Example 2 ○ 52.2 2.26 7.1 120 93 Comparative Example 3 ○ 11.5 0.25 950 170 82.4 Comparative Example 4 X N.A N.A N.A 130 91.5 Comparative Example 5 ○ 21 0.15 333 130 93.2 Comparative Example 6 ○ 18 0.99 314 120 92.9 Example 1 ○ 11.0 0.15 302 140 75 Example 2 ○ 32.4 0.425 700 150 73.5 Example 3 ○ 10.9 0.285 667 135 76 Example 4 ○ 29.9 0.409 785 130 75.2 Example 5 ○ 39.13 2.25 1.99 120 94.2 Example 6 ○ 10.16 0.02 578 140 92.7 Example 7 X N.A N.A N.A 110 95.2 Example 8 ○ 9.81 0.02 557 170 92.1 Example 9 ○ 2.9 0.02 157 180 91.7 *N.A not measured - Comparing Comparative Example 3 with Examples 2 and 4, Examples 2 and 4 showed that through a block copolymerization between poly(3-hydroxypropionic acid) and caprolactam, the tensile strength was increased to 20 MPa or more and the elongation was significantly increased to 600% or more. In particular, Examples 2 and 4, in which a weight average molecular weight was 100,000 g/mol or more, were excellent in both strength and elongation. Example 1 had the same monomer composition, catalyst type, use amount, and reaction temperature as Example 2, but the reaction time was 3 hours, which had a shorter reaction time than Example 2. Therefore, the tensile strength and elongation of Example 1 were shown inferior to those of Example 2, which is because the molecular weight of Example 1, which has a short reaction time, is small and thus entanglement between chains is small. Example 3 also had the same monomer composition, catalyst type, use amount and reaction temperature as Example 4, but the reaction time was 3 hours which is the shorter reaction time than Example 4. Therefore, the tensile strength and elongation of Example 3 were showed inferior to those of Example 4, which is because the molecular weight of Example 3, which also has a short reaction time, is small and thus entanglement between chains is small.
- Comparing Comparative Example 4 and Example 5, it was confirmed that in Example 5, butyrolactone was block-copolymerized with poly (3-hydroxypropionic acid), and thus, the thermal processability was improved as compared to Comparative Example 4 in which thermal processing was impossible due to its brittleness. In addition, in Example 5, the copolymerized butyrolactone had a harder property than lactide, and thus the elongation was measured to be very low.
- Comparing Comparative Examples 5 and 6 with Examples 6 to 9, it can be confirmed that in addition to caprolactone and lactide, poly(3-hydroxypropionic acid) was copolymerized, and thus, elongation increased from 300% to 600% while maintaining transparency. However, in the case of the sample without crystallinity in Example 7, it showed the same behavior as a gum at room temperature, which makes it difficult to make a dog-bone, and thus, the mechanical properties could not be confirmed. In the case of Example 9, the dog-bone could be manufactured, but is low in crystallinity, defects occurred during the manufacture of the dog-bone, resulting in low mechanical properties.
- In addition, comparing Examples 6 and 8 and Examples 7 and 9, it was confirmed that the tensile strength and elongation could be controlled by adjusting the lactone and lactide mixing ratio. It was confirmed that the processability, strength, and elongation can be adjusted depending on whether the structure is random or block.
Claims (13)
- A poly(3-hydroxypropionic acid) block copolymer, comprising:a repeating unit of the following Chemical Formula 1, which is a repeating unit of 3-hydroxypropionic acid; anda repeating unit of the following Chemical Formula 2, which is a repeating unit of lactone,wherein the number (m) of repeating units of the Chemical Formula 1 is an integer of 100 to 5000,wherein the number (n) of repeating units of the Chemical Formula 2 is an integer of 100 to 5000, and
- The poly(3-hydroxypropionic acid) block copolymer according to claim 1 wherein:
the poly(3-hydroxypropionic acid) block copolymer further comprises:a repeating unit represented by the following Chemical Formula 3, which is a repeating unit of a lactide, - A method of manufacturing a poly(3-hydroxypropionic acid) block copolymer, comprising the steps of:polymerizing 3-hydroxypropionic acid to produce a 3-hydroxypropionic acid oligomer (step 1);polymerizing the 3-hydroxypropionic acid oligomer to produce poly(3-hydroxypropionic acid) (step 2); andperforming a ring-opening polymerization of lactone having 3 to 10 carbon atoms using the poly(3-hydroxypropionic acid) as an initiator (step 3).
- The method of claim 3, wherein:
the (step 3) further includes adding a lactide as a monomer. - The method of claim 4, wherein:
the lactide is included in an amount of 40 parts by weight to 99 parts by weight based on 100 parts by weight of the total weight of lactone and lactide. - The method of claim 3, wherein:
in the (step 3), the poly(3-hydroxypropionic acid) is included in an amount of 50 parts by weight or less based on 100 parts by weight of the total weight of the reactants. - The method of claim 3, wherein:
the lactone having 3 to 10 carbon atoms of the (step 3) is at least one selected from the group consisting of ε-caprolactone, β-butyrolactone, β-valerolactone, γ-butyrolactone, δ-valerolactone, γ-valerolactone, trimethylenecarbonate, p-dioxanone, δ-haxalactone, δ-caprolactone, mevalonolactone, γ-octanoic lactone, and γ-nonanoic lactone. - The method of claim 3, wherein:
polymerizing the 3-hydroxypropionic acid oligomer in the (step 2) is done under a pressure condition of 1 torr or less. - The method of manufacturing a poly(3-hydroxypropionic acid) block copolymer according to claim 3, wherein:
performing the ring-opening polymerization in the (step 3) is done at a temperature of 140 to 190°C. - A resin, comprising the poly(3-hydroxypropionic acid) block copolymer as set forth in claim 1.
- A resin composition, comprising the resin as set forth in claim 10.
- The resin composition according to claim 11, wherein:
the resin composition is molded into one or more resin molded articles selected from the group consisting of an injection molded article, an extrusion molded article, a blow molded article, an inflation molded article, a fiber, a nonwoven fabric, a foam, a sheet, and a film. - An article, comprising the poly(3-hydroxypropionic acid) block copolymer as set forth in claim 1.
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EP22853485.5A Pending EP4357386A1 (en) | 2021-08-04 | 2022-08-04 | Poly(3-hydroxypropionic acid) block copolymer, preparation method therefor and product comprising same |
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EP (1) | EP4357386A1 (en) |
JP (1) | JP2024525890A (en) |
WO (1) | WO2023014109A1 (en) |
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JPS58111870A (en) * | 1981-12-25 | 1983-07-04 | Nippon Oil & Fats Co Ltd | Antifouling coating |
KR102088504B1 (en) * | 2015-09-03 | 2020-03-12 | 주식회사 엘지화학 | Copolymer comprising 3-hydroxypropionate, 2-hydroxybutyrate and lactate as repeating unit and method for preparing the same |
KR102539511B1 (en) * | 2019-03-26 | 2023-06-02 | 주식회사 엘지화학 | Process for preparation of block copolymer |
KR20210102547A (en) | 2020-02-11 | 2021-08-20 | 두산중공업 주식회사 | White smoke reduction device, white smoke reduction cooling tower and white smoke reduction method |
KR20220096678A (en) | 2020-12-31 | 2022-07-07 | 이경숙 | Mat with harmful electromagnetic waves protecting function |
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2022
- 2022-08-04 JP JP2024503472A patent/JP2024525890A/en active Pending
- 2022-08-04 WO PCT/KR2022/011553 patent/WO2023014109A1/en active Application Filing
- 2022-08-04 EP EP22853485.5A patent/EP4357386A1/en active Pending
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WO2023014109A1 (en) | 2023-02-09 |
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